2014
DOI: 10.1002/pen.23883
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Numerical simulation and experimental study of pressure and residence time distribution of triple‐screw extruder

Abstract: Three-dimensional flow field of triangle arrayed triplescrew extruder (TTSE) in different feed rates, screw speeds and screw configurations were simulated by POLYFLOW. Polypropylene processing by TTSE was tested to validate the numerical simulation. The reliability of simulation was tested directly and indirectly by comparing the axial pressure difference and residence time distribution (RTD) separately. The results show that the axial pressure differences from the simulations and experiments were in high agre… Show more

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Cited by 15 publications
(10 citation statements)
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“…The materials firstly flow through the high shear region composed of three meshing zones to achieve distributive mixing, then enter the central area where melt stretching and dispersive mixing will be achieved. The whole process formed alternating shearing and extensional flow field, contributing to the efficient dispersion and mixing of the materials . However, the flow field in the twin screw extruder is usually dominated by the shear flow .…”
Section: Introductionmentioning
confidence: 99%
“…The materials firstly flow through the high shear region composed of three meshing zones to achieve distributive mixing, then enter the central area where melt stretching and dispersive mixing will be achieved. The whole process formed alternating shearing and extensional flow field, contributing to the efficient dispersion and mixing of the materials . However, the flow field in the twin screw extruder is usually dominated by the shear flow .…”
Section: Introductionmentioning
confidence: 99%
“…Additionally, published data indicate that in triplescrew extruders the power consumption is 1.5 times higher than in co-rotating twin-screw extruders, while simultaneously their productivity increase around 1.3 times [34]. However, despite of above mentioned advantages of triple screw extrusion the research works about its application in polymer technology are still very limited [35][36][37], while its using during reactive processing is practically unknown. This is due to its high costs related to complicated screw geometry and barrel construction, comparing to single-or twin-screw extruders.…”
Section: Extruders As Chemical Reactors -Basic Conceptsmentioning
confidence: 99%
“…To valid the numerical model, RTD experiment with calcined tracer was usually performed . The geometry of extruder (HT‐30, Nanjing Rubber and Plastics Machinery Plant Co., Ltd., China) were show in Fig.…”
Section: Numerical Simulationmentioning
confidence: 99%